Method And Apparatus For Producing Liquid Nitrogen Fertilizer And Plasma Activated Water

ABSTRACT

The invention relates to a method and apparatus for in situ production of liquid nitrogen fertilizer and plasma activated water for agricultural nutrient management and irrigation water treatment. In the invention, there are two different kinds of plasma reactors operates in tandem.

TECHNICAL FIELD

The invention relates to a method and apparatus for in situ production of liquid nitrogen fertilizer and plasma (ionized gas) activated water reactive for agricultural nutrient management and irrigation water treatment.

PRIOR ART

Nitrogen fixation, conversion of unreactive nitrogen gas in the air into more reactive compounds of nitrogen in soil, is essential to the growth of plants and life on Earth. The Birkeland-Eyde process was an industrial process to fixate nitrogen by passing air through an electric arc to produce synthetic nitrates until it was replaced by the Haber-Bosch (H-B) process.

The H-B process relies on fossil fuels, and has massive carbon footprint accounting for 1% of global annual CO₂ emissions and 2% of the world energy consumption. [1] Ammonia-based fertiliser production via the H-B process is highly centralized, while the consumption is dispersed globally in agricultural areas. The need for transportation therefore further increases greenhouse gas emissions, and associated costs, and limit distribution resulting in inability to enrich soils in remote and impoverished regions. Also, the overall process of fertilizer application is quite inefficient due to leaching of a large amount of nitrogen content from soil, which fouls ground water in the form of nitrates, and enter the atmosphere as nitrous oxide, a greenhouse gas 300 times worse than carbon dioxide. The nitrogen retention after excessive fertilizer usage could damage the soil and ground water health as well.

There is a need for developing new sustainable and distributed approaches for fixing nitrogen. During the last two decades non-thermal plasma in contact with liquids as an alternative to the electric arc (thermal plasma) process have received a lot of attention for in situ nitrogen fixation. Although state-of-the-art plasma reactors cannot compete with the H-B process in terms of energy efficiency and product yield (despite the fact that theoretical limit of energy consumption for non-thermal plasma-based process is lower than the limitation of H-B process [2]), plasma-based process is the enabling technology for small-scale, on-demand and decentralized fertilizer production, and has the advantage of integration with renewable energy, making the process sustainable. On-demand production coupled with precision-farming techniques, the inefficiency and environmental pollution of the fertilizer application may also be remedied.

For example, decentralized and small-scale production may resolve the bottleneck around nitrogen fertilizer supply in sub-Saharan Africa (SSA). Fertilizer consumption, and thus crop yields, in SSA remains the lowest when compared with other regions due to high retail prices related to transportation costs and poor management of subsidy programs. [3] Fertilizers need to be transported across great distances making it so expensive outweighing the benefits of using them. The subsidy programs have often been poorly managed to help smallholder farmers on a sustained basis most severely affecting smallholder farmers, the poorest members of society. There is a great demand for affordable nitrogen fertilizer as being unable access to nitrogen fertilizer is a key impediment in increasing agricultural production and incomes of smallholder farmers in SSA.

Plasma can react with air and treat water or “activate” to produce reactive nitrogen and oxygen compounds (e.g. nitric oxide and hydrogen peroxide) merely by the use of air, water and electricity. The resultant plasma activated water (PAW) is an effective liquid nitrogen fertilizer (as it typically contains nitrates and nitrites) and broad-spectrum biocidal agent. It may enhance seed germination, increase rooting speed, stimulate plant growth, prevent pests and disinfect wastewater. [4] PAW may increase plant uptake, and thus fertilizer use efficiency, because plants absorb nitrogen from the soil as nitrate and ammonium ions. It may also significantly reduce losses of nitrogen content in soil or organic waste by converting volatile ammonia into involatile ammonium as described in CA 2851348.

U.S. Pat. No. 4,297,123 describes a method and apparatus for small scale and on-site production of nitrate fertilizers in various forms. Nitrogen dioxide is produced from air, which passed through an electric arc occurs between the electrodes of a spark plug, and absorbed in water to make nitric acid, which dissociates into nitrate in water.

U.S. Pat. No. 8,951,481 describes a system for creating a nitrate combined with a liquid in which nitrogen dioxide is produced by passing air through a corona discharge cell. The nitrogen dioxide is injected into a water chamber to generate nitric acid.

U.S. Pat. No. 4,915,915 describes a system for nitrogen fertilizer using an electric arc process in which the electric arc necessary for the process is generated by piezoelectric elements actuated by a hammer mechanism powered by water pressure.

U.S. Pat. No. 7,992,641 describes a method and apparatus for on-site production of nitrate ions by an electric arc process in a water processing system to reduce the number of sulfate-reducing-bacteria in oil and gas reservoirs.

WO 2016/096751 describes a thermal and non-thermal plasma activated water reactor system to produce plasma activated water (PAW).

Prior art has not been able to cost-effectively scale down the electric arc process, whereas non-thermal plasma reactor designs have low fixed nitrogen throughput, and require expensive power supplies. For economic viability, energy efficiency of aqueous nitrogen compound production by plasma-based process should be increased one order of magnitude, and a no/low-maintenance plasma reactor system should be designed.

Aims of the Invention and Brief Description

The main purpose of this invention is to produce aqueous nitrogen compounds such as nitrate (NO³⁻) and nitrite (NO²⁻) containing liquid nitrogen fertilizer and plasma (ionized gas) activated water.

The object of the present invention is to provide an energy efficient high throughput method and a low-cost low-maintenance mobile apparatus to make nitrogen fertilizers more accessible to smallholder farmers reducing the reliance on resource and capital intensive fertilizer factories and associated high-cost distribution networks.

To provide a solution to the above-mentioned challenges, a method and apparatus is provided that includes two different kinds of plasma reactors operating in tandem. Having cylindrical electrodes concentrically aligned with a dielectric tube (8), the primary plasma reactor (5) has two discharge channels (10,12) providing stable dielectric barrier discharge and relatively larger discharge area. A large discharge area is desirable not only for higher yield of NOx gases but also for more uniform heat distribution on the electrode (9,11) surfaces increasing the lifetime i.e. lower material erosion. The secondary plasma reactor (17) produces plasma discharge between upper and lower liquid electrodes (21, 22), which eliminates the electrode erosion problem of plasma reactors with metal electrodes, prevents toxic metal contamination due to the electrode erosion, and reduces maintenance costs.

The upper liquid electrode (21) of the secondary plasma reactor (17) comprises of multiple liquid droplets providing relatively larger area of gas-liquid interface for improved absorption rate of discharge by products.

The apparatus uses an absorption unit in coil structure (27), which is a long length of plastic tubing shaped into a coil, to enhance NOx gas absorption in the lower liquid electrode (22). There are multiple swirlers (29) or static mixers within the absorption coil plastic tube to increase absorption yield.

Recirculation of the liquid flow in the secondary plasma reactor (17) leads to greater transport rate of the reactive oxygen and nitrogen species (ROS and RNS) into the liquid water due to increased interaction between plasma discharges and liquid water.

NOx gas absorption in liquid water is quite difficult compared to other exhausted gas such as NH₃ due to its low water solubility. Efficiency of NOx gas absorption is increased by generating and mixing hydrogen peroxide in the absorption liquid and recirculating it in the absorption coil (27). Ozone oxidation in liquid water or lower liquid electrode (22) of the secondary plasma reactor (17) can convert NO gas, which has low water solubility, to the more soluble NO₂ gas. Water dissolved ozone can convert nitrous acid to nitric acid in the water phase. Nitric acid dissociates into nitrate in lower liquid electrode (22).

A slow but continuous fertilization and irrigation routine is adopted. The apparatus may include a control unit to control and monitor air compressor, liquid pumps, power supplies and concentration of nitrogen-containing compounds and oxygen-containing compounds generated in primary and secondary plasma reactors.

DEFINITION OF THE FIGURES OF THE INVENTION

Features of the present invention may be better understood with reference to the drawings described below. The drawings are not necessarily to scale; emphasis instead generally being placed upon illustrating the principles of the invention.

FIG. 1: An embodiment of the invention with primary plasma reactor, secondary plasma reactor and absorption coil.

FIG. 2: Flow chart, illustrating a method for in situ production of liquid nitrogen fertilizer and plasma (ionized gas) activated water reactive, according to one embodiment of the present invention.

FIG. 3: An image of plasma discharge filaments formed between electrodes.

DEFINITIONS OF THE PARTS/ASPECTS/SECTIONS FORMING THE INVENTION

-   1: Air Source -   2: Air Compressor -   3: Air Dehumidifier Filter -   4: Gas Inlet Port -   5: Primary Plasma Reactor -   6: Body Structure -   7: Enclosing Structure -   8: Dielectric Tube -   9: Inner Electrode, -   10: Inner Discharge Channel -   11: Outer Electrode -   12: Outer Discharge Channel -   13: Gas Outlet Port -   14: Cooling Unit -   15: Filter Unit -   16: Liquid Inlet Port -   17: Secondary Plasma Reactor -   18: Bubble Diffuser -   19: Fine Bubble -   20: Droplet Generator -   21: Upper Liquid Electrode -   22: Lower Liquid Electrode -   23: Liquid Inlet Port -   24: Liquid Outlet Port -   25: Liquid Pump -   26: Power Supply -   27: Absorption Coil -   28: Venturi -   29: Swirler -   30: Valve -   31: Drip Irrigation Pipe

DETAILED DESCRIPTION OF THE INVENTION

An apparatus for producing liquid nitrogen fertilizer and plasma activated water, comprising;

a) A primary plasma reactor (5) to convert air to reactive oxygen and nitrogen species (ROS and RNS) such as nitrogen oxides (NOx) and ozone, wherein said primary plasma reactor (5) comprises an inner annular-shaped discharge channel (10) and an outer annular-shaped discharge channel (12) to treat air; an inner electrode preferably anodized metal mesh electrode (9) and an outer electrode preferably anodized metal mesh electrode (11) which provide electric field for ionization of air; a gas outlet port (13) to release air containing discharge products. b) A secondary plasma reactor (17) to convert air and water vapor to reactive oxygen and nitrogen species (ROS and RNS), wherein said secondary plasma reactor (17) comprises a liquid pump (25), which recirculates a liquid flow between a liquid outlet port (24) and a liquid inlet port (23); a liquid outlet port (24) to remove liquid water; liquid inlet port (23) to supply liquid water to the droplet generator; a gas outlet port (13) to release treated air; an electrically conductive lower liquid electrode (22) and an electrically conductive upper liquid electrode (21) to provide electric field for ionization of air and water vapor; a liquid drop or droplet generator (20) to generate water droplets, where the liquid drop or droplets serve as the upper liquid electrode (21). c) At least one absorption coil (27) to increase efficiency of NOx gas absorption, wherein said absorption coil (27) comprises a liquid pump (25), which recirculates a liquid flow between a liquid outlet port (24) and a liquid inlet port (23); liquid outlet port (24) to remove liquid water, a liquid inlet port (23) to supply liquid water into the absorption coil (27), and at least one swirler (29) to improve air and water mixing. Lower liquid electrode (22) of secondary plasma reactor (17) is liquid water recirculated in the absorption coil (27).

A preferred embodiment of the present invention may be understood with reference to FIG. 1. An air compressor (2) takes air comprising nitrogen, oxygen and other gaseous elements from an air source (1), passes it through an air dehumidifier filter (3), and delivers dried air to a primary plasma reactor (5).

Primary plasma reactor (5) comprises a gas inlet port (4), which supply air from an air source (1), a body structure (6), which also serves as air distributor, an airtight enclosing structure (7) to enclose the body structure (6), which includes heat sink and cooling fins, an inner annular-shaped discharge channel (10), an outer annular-shaped discharge channel (12), an inner electrically conductive electrode (9), an outer electrically conductive electrode (11), a dielectric tube (8), a gas outlet port (13) and high voltage high frequency alternating current (AC) power supply (26), which biases said inner and outer electrodes (9,11).

Electrodes of primary and secondary plasma reactors (5, 17) are connected to at least one power supply which is selected from group of high voltage high frequency alternating current (AC) supply, high voltage direct current (DC) power supply, pulsed AC power supply, pulsed DC power supply or any combination thereof, to provide electric field for ionization of gases in the plasma reactors. Power supplies for primary and secondary plasma reactors (5, 17) can be same type or different type.

Absorber coil (27) and secondary plasma reactor is a set and the apparatus comprise at least one set, wherein gas outlet port (13) is connected to another set of absorber coil (27) and secondary plasma reactor (17). In another embodiment, number of sets is at least two. In general, a method of producing liquid nitrogen fertilizer and plasma activated water comprises following steps:

-   -   Delivering air to an electric arc, dielectric barrier discharge,         nanosecond pulsed electric field, or electromagnetic wave driven         primary plasma reactor, or any combination thereof, to ionize         and decompose nitrogen and oxygen molecules in air into the         constituent atoms to form nitric oxide, nitrogen dioxide and         ozone gases,     -   Feeding the air containing nitric oxide, nitrogen dioxide and         ozone gases to an absorption unit, and absorbing the discharge         byproducts into an absorption liquid in the absorption unit to         form nitrous acid and nitric acid solution,     -   Activation of the absorption liquid to produce hydrogen         peroxide, hydroxyl radical and ozone by an electric arc,         dielectric barrier discharge, nanosecond pulsed electric field,         or electromagnetic wave driven secondary plasma reactor to         increase absorption efficiency through reaction of the nitrogen         dioxide gas with hydrogen peroxide in the absorption liquid to         form nitric acid,     -   Reaction of nitrogen dioxide and nitric oxide with hydroxyl         radical to form nitric acid and nitrous acid,     -   Reaction of nitrogen molecules in air and the absorption liquid         with ozone to form nitrous acid,     -   Reaction of nitrous acid with ozone to form nitric acid,     -   Dissociation of nitric acid into nitrate and nitrous acid into         nitrite in the plasma activated liquid,     -   Providing the nitrite and nitrate containing plasma activated         water for crop fertilization and irrigation.

FIG. 2 summarizes a method of producing liquid nitrogen fertilizer and plasma activated water with the apparatus comprises following steps;

-   -   To be taken of air comprising nitrogen, oxygen and other gaseous         elements from an air source (1) by an air compressor (2),     -   Delivering dried air to a primary plasma reactor (5),     -   Ionization and decomposition of nitrogen and oxygen molecules in         air into the constituent atoms to form reactive oxygen and         nitrogen species (ROS and RNS) in the discharge channels (10,12)         due to application of a strong electric field between the inner         and outer electrodes (9,11),     -   Below chemical reactions where the reactions are only the major         reactions and are not limiting,     -   Introducing air containing discharge byproduct gases nitric         oxide, nitrogen dioxide and ozone gases from the gas outlet port         (13) into a venturi (28) within the output line of a liquid pump         (25), which recirculates a lower liquid electrode (22) between a         liquid outlet port (24) and a liquid inlet port (16) to form an         acidic nitrogen solution comprising nitrates and nitrites         through 2NO₂+H₂O→HNO₂+HNO₃,     -   Nitric acid dissociates into nitrate, and nitrous acid         dissociates into nitrite in lower liquid electrode (22) through         the reactions HNO₃+H₂O         H₃O⁺+NO₃ ⁻ and HNO₂+H₂O         H₃O⁺+NO₂ ⁻,     -   Conversion of nitrogen molecules in air and ozone in absorption         lower liquid electrode (22) to nitrous acid through the reaction         N₂+O₃+H₂O→2HNO₂,     -   Conversion of nitrous acid to nitric acid in the water phase         through the reaction HNO₂+O₃→HNO₃+O₂,     -   Conversion of nitric oxide to nitrogen dioxide through the         reaction NO+O₃→NO₂+O₂,     -   Plasma activation of water and generation of reactive oxygen         species in a secondary plasma reactor (17),     -   Mixing of hydrogen peroxide with the absorption lower liquid         electrode (22) and recirculating it in the absorption coil (27)         to increase absorption efficiency of nitrogen dioxide in liquid         water (and thus nitric acid concentration) through the reaction         2NO₂+H₂O₂→2HNO₃,     -   Conversion of nitric oxide and nitrogen dioxide to nitrous acid         and nitric acid through the reactions: NO+OH→HNO₂, NO₂+OH→HNO₃.

As the air travels through the discharge channels (10,12), nitrogen and oxygen molecules are ionized, and decomposed into the constituent atoms to form reactive nitrogen species (RNS) such as nitrogen oxides (NOx gases) in the discharge channels (10,12) due to application of a strong electric field between the inner and outer electrodes (9,11). A filter unit (15) is configured to remove any structural fragments coming from the plasma discharge channels due to erosion or to selectively pass discharge byproduct gases to control plasma chemistry. Cooling unit (14) serve to cool down the primary plasma reactor (5) and the power supplies (26).

In order to form an acidic nitrogen solution comprising nitrates and nitrites through the chemical reaction 2NO₂+H₂O→HNO₂+HNO₃, the air containing NOx gases and other discharge byproduct gases are introduced to a venturi (28) through the gas outlet port (13) within the output line of a liquid pump (25), which recirculates a lower liquid electrode (22) between a liquid outlet port (24) and a liquid inlet port (16). An absorption coil (27), which includes a liquid inlet port (23), liquid outlet port (24) and a series of swirlers (29) or static mixers to provide substantial gas-liquid exposure. The liquid outlet port (24) is connected to a secondary plasma reactor (17) through the liquid inlet port (16).

The secondary plasma reactor (17) includes a liquid pump (25), which recirculates a liquid flow between a liquid outlet port (24) and a liquid inlet port (23), a gas outlet port (13), a bubble diffuser (18) to form fine bubbles (19), an electrically conductive liquid lower electrode (22), a liquid drop or droplet generator (20), where the liquid drop or droplets serve as upper liquid electrode (21), and high voltage high frequency AC power supply (26), which biases said electrodes.

Electrical breakdown of water vapor and air due to strong electric field in the gap between the two electrode surfaces (21, 22) of the secondary plasma reactor (17) develop luminous plasma discharge filaments, which activate/treat water, and produce reactive oxygen species (ROS) due to presence of liquid water and water vapor and reactive nitrogen species (RNS) due to presence of nitrogen gas in the air delivered to the secondary plasma reactor (17). Plasma discharge filaments in the secondary plasma reactor (17) extinguish and regenerate continuously as water drops encounters surface of the lower liquid electrode (22), and the droplet generator (20) creates new water drops. An embodiment of the invention has been tested. A multiple number of plasma discharge filaments form between the two electrode surfaces (21, 22) as shown in FIG. 3.

Some reactive oxygen species generated in the secondary plasma reactor (17) are short-lived hydroxyl radical and long-lived hydrogen peroxide, which increase the absorption efficiency of NO₂ in water and nitric acid concentration through the reactions: NO+OH→HNO₂, NO₂+OH→HNO₃, 2NO₂+H₂O₂→2HNO₃. Nitric acid dissociates into nitrate in lower liquid electrode (22) through the reaction HNO₃+H₂O→H₃O⁺+NO₃ ⁻.

Another reactive oxygen species generated in both primary plasma reactor and secondary plasma reactor (17) is ozone. Ozone oxidation in liquid water or lower liquid electrode (22) can convert NO gas, which has low water solubility, to the more soluble NO₂ gas through the reaction NO+O₃→NO₂+O₂. Water dissolved ozone can convert nitrous acid to nitric acid in the water phase through the reaction HNO₂+O₃→HNO₃+O₂. Nitric acid dissociates into nitrate in lower liquid electrode (22) through the reaction HNO₃+H₂O→H₃O⁺+NO₃ ⁻.

Remaining nitrogen gases that are not fixed in the secondary plasma reactor (17) may be fed back into the primary plasma reactor (5) or released into atmosphere by the gas outlet port (13) after passing through a filter unit (not shown in FIG. 1). In another embodiment, the remaining gases may be directed by the gas outlet port (13) to another set of absorption coil (27) and a plasma reactor similar to the secondary plasma reactor (17).

A liquid outlet port (24), which is controlled by a valve (30), connect the secondary plasma reactor (17) to a venturi (28) to mix the aqueous nitrite and nitrate solutions and plasma activated water to drip irrigation pipes (31).

A liquid pump, which is not shown, is used to fill or empty the secondary plasma reactor (17). A valve, which is not shown, is placed within the input line of venturi (28), to assure that no liquid can flow backwards, and enter the primary plasma reactor (5). The apparatus is placed in a sheet metal cabinet to shield electromagnetic interference radiation. One can modify induced plasma chemistry e.g. concentration of NOx in the primary plasma reactor (5) or ROS and RNS in the secondary plasma reactor (17) by tailoring air pressure, treatment time, voltage, current, frequency or duty cycle of the high voltage high frequency power supplies (26) and water treatment time. Electrical energy to drive the apparatus may be obtained from mains, portable electric generators or renewable sources such as solar panels and wind turbines.

In one embodiment of the invention, the secondary plasma reactor (17) can include a mist maker, preferably ultrasonic mist maker in order to enhance generation of reactive species by spraying water mist into plasma discharge region. In another embodiment, a plurality of the primary plasma reactor (5) can be connected in series or parallel to the same the absorber coil (27) and/or plurality of the secondary plasma reactor (17) can be connected in series or parallel to the same absorber coil (27) to increase the amount of nitrate in the lower liquid electrode (22). In yet another embodiment, potash and phosphate containing materials may be added to the lower liquid electrode (22) according to the desired fertilizer characteristics.

The apparatus may be portable, and used to deploy the produced liquid fertilizer directly to a crop/plant. The nitrogen fertilizer may be used as it is produced by spraying, fed into the drip irrigation system or incorporated into a hydroponic system. Calcium carbonate (CaCO₃) may be added to the produced liquid nitrogen fertilizer and plasma activated water to convert nitric acid to calcium nitrate fertilizer through the chemical reaction CaCO₃+2HNO₃→H₂O+CO₂+Ca(NO₃)₂, and use when needed.

REFERENCES

-   [1] Smil, V. (2004). Enriching the Earth: Fritz Haber, Carl Bosch,     and the Transformation of World Food Production. Cambridge, MIT     Press. -   [2] Li, S. et al. (2018). Recent Progress of Plasma-Assisted     Nitrogen Fixation Research: A Review. Processes 2018, 6(12), 248. -   [3] Druilhe, Z. & Barreiro-Hurlé, J. (2012). Fertilizer Subsidies in     sub-Saharan Africa. ESA Working Paper No. 12-04. -   [4] Park, D. P. et al. (2013). Reactive Nitrogen Species Produced in     Water by Non-Equilibrium Plasma Increase Plant Growth Rate and     Nutritional Yield. Curr. Appl. Phys. 13, S19-S29. 

What is claimed is:
 1. An apparatus for producing liquid nitrogen fertilizer and plasma activated water, comprising; a) A primary plasma reactor to convert air to reactive oxygen and nitrogen species (ROS and RNS) such as nitrogen oxides (NOx) and ozone, wherein said primary plasma reactor comprises an inner annular-shaped discharge channel and an outer annular-shaped discharge channel to treat air; an inner electrode and an outer electrode; a gas outlet port to release air containing discharge byproducts. b) A secondary plasma reactor to convert air and water vapor to reactive oxygen and nitrogen species (ROS and RNS), wherein said secondary plasma reactor comprises a liquid pump, which recirculates a liquid water flow between a liquid outlet port to remove water and a liquid inlet port to supply liquid water to the droplet generator; a gas outlet port to release treated air; a lower liquid electrode; a liquid water drop or droplet generator to create water droplets, where the liquid drop or droplets serve as upper liquid electrode. c) at least one absorption coil to increase efficiency of NOx gas absorption, wherein said absorption coil comprises a liquid pump, which recirculates a liquid flow between a liquid outlet port and a liquid inlet port; liquid outlet port to remove liquid water, a liquid inlet port to supply liquid water into the absorption coil, and at least one swirler to improve air and water mixing.
 2. The apparatus for producing liquid nitrogen fertiliser and plasma activated water according to claim 1, wherein said primary plasma reactor further comprises a gas inlet port which supplies air from an air source by an air compressor.
 3. The apparatus for producing liquid nitrogen fertiliser and plasma activated water according to claim 1, wherein said primary plasma reactor further comprises an air dehumidifier filter.
 4. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said primary plasma reactor further comprises a body structure, which also serves as air distributor.
 5. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said primary plasma reactor further comprises an airtight enclosing structure with heat sink fins which enclose the body structure making discharge channels airtight.
 6. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said primary plasma reactor further comprises a filter unit configured to remove any structural fragments coming from the plasma discharge channels or to selectively pass discharge byproduct gases.
 7. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said primary plasma reactor further comprises a cooling unit to cool down the primary plasma reactor and power supply.
 8. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said electrodes of primary and secondary plasma reactors are connected to at least one power supply which is selected from group of high voltage high frequency alternating current (AC) supply, high voltage direct current (DC) power supply, pulsed AC power supply, pulsed DC power supply or any combination thereof, to provide electric field for ionization of gases in the plasma reactors.
 9. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 8 where power supplies for primary and secondary plasma reactors are same type or different type.
 10. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said secondary plasma reactor further comprises a bubble diffuser to form fine bubbles.
 11. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein said secondary plasma reactor further comprises a mist maker in order to enhance generation of reactive oxygen and nitrogen species.
 12. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein a plurality of said primary plasma reactor are connected in series or parallel to the absorber coil.
 13. The apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1, wherein absorber coil and secondary plasma reactor is a set and the apparatus of claim 1 comprise at least one set, said gas outlet port is connected to another set of absorber coil and secondary plasma reactor.
 14. Apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 13, where number of said set is at least two.
 15. Apparatus for producing liquid nitrogen fertilizer and plasma activated water according to claim 1 further comprises a control unit.
 16. A method of producing liquid nitrogen fertilizer and plasma activated water comprising steps of Delivering air to an electric arc, dielectric barrier discharge, nanosecond pulsed electric field, or electromagnetic wave driven primary plasma reactor, or any combination thereof, to ionize and decompose nitrogen and oxygen molecules in air into the constituent atoms to form nitric oxide, nitrogen dioxide and ozone gases, Feeding the air containing nitric oxide, nitrogen dioxide and ozone gases to an absorption unit, and absorbing the discharge byproducts into an absorption liquid in the absorption unit to form nitrous acid and nitric acid solution, Activation of the absorption liquid to produce hydrogen peroxide, hydroxyl radical and ozone by an electric arc, dielectric barrier discharge, nanosecond pulsed electric field, or electromagnetic wave driven secondary plasma reactor to increase absorption efficiency through reaction of the nitrogen dioxide gas with hydrogen peroxide in the absorption liquid to form nitric acid, Reaction of nitrogen dioxide and nitric oxide with hydroxyl radical to form nitric acid and nitrous acid, Reaction of nitrogen molecules in air and the absorption liquid with ozone to form nitrous acid, Reaction of nitrous acid with ozone to form nitric acid, Dissociation of nitric acid into nitrate and nitrous acid into nitrite in the plasma activated liquid, Providing the nitrite and nitrate containing plasma activated water for crop fertilization and irrigation. 